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    PRODUCTION OF BASE OILS FROM PETROLATUM
    33.
    发明申请
    PRODUCTION OF BASE OILS FROM PETROLATUM 有权
    从石蜡生产基础油

    公开(公告)号：US20160152914A1

    公开(公告)日：2016-06-02

    申请号：US15019225

    申请日：2016-02-09

    Applicant: ExxonMobil Research and Engineering Company

    Inventor： Jeenok T. Kim ,  Gary P. Schleicher ,  Halou Oumar-Mahamat ,  Chad H. Mondor

    IPC: C10M101/02

    CPC classification number: C10M101/02 ,  C10G21/003 ,  C10G45/02 ,  C10G45/06 ,  C10G45/08 ,  C10G45/58 ,  C10G45/62 ,  C10G45/64 ,  C10G47/00 ,  C10G47/04 ,  C10G47/16 ,  C10G65/043 ,  C10G67/0454 ,  C10G69/02 ,  C10G69/04 ,  C10G73/06 ,  C10G73/44 ,  C10G2300/1062 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/304 ,  C10G2400/10 ,  C10M1/00 ,  C10M2203/1025 ,  C10N2220/022 ,  C10N2230/02

    Abstract: Methods are provided for producing lubricant base oils from petrolatum. After solvent dewaxing of a brightstock raffinate to form a brightstock base oil, petrolatum is generated as a side product. The petrolatum can be hydroprocessed to form base oils in high yield. The base oils formed from hydroprocessing of petrolatum have an unexpected pour point relationship. For a typical lubricant oil feedstock, the pour point of the base oils generated from the feedstock increases with the viscosity of the base oil. By contrast, lubricant base oils formed from hydroprocessing of petrolatum have a relatively flat pour point relationship, and some of the higher viscosity base oils unexpectedly have lower pour points than lower viscosity base oils generated from the same petrolatum feed. The base oils from petrolatum are also unusual in yielding both high viscosity and high viscosity index and can be generated while maintaining a high yield.

    Abstract translation: 提供从凡士林生产润滑油基础油的方法。 在明亮的原料萃余液的溶剂脱蜡后，形成光油基础油，产生凡士林作为副产物。 可以加氢处理矿脂以高产率形成基础油。 由凡士林加氢处理形成的基础油具有意想不到的倾点关系。 对于典型的润滑油原料，由原料产生的基础油的倾点随着基础油的粘度而增加。 相比之下，通过加氢处理矿脂形成的润滑剂基础油具有相对平坦的倾点关系，并且一些较高粘度的基础油意外地具有比由相同凡士林饲料产生的低粘度基础油更低的倾点。 来自凡士林的基础油在产生高粘度和高粘度指数方面也是不寻常的，并且可以在保持高产率的同时产生。

    Process to prepare a microcystalline wax and a middle distillate fuel
    35.
    发明申请
    Process to prepare a microcystalline wax and a middle distillate fuel 失效
    制备微晶蜡和中间馏分燃料的方法

    公开(公告)号：US20050247601A1

    公开(公告)日：2005-11-10

    申请号：US10521668

    申请日：2003-07-17

    Applicant: Arend Hoek

    Inventor： Arend Hoek

    IPC: C10G65/12 ,  C10G45/58 ,  C10G45/62 ,  C10G47/14 ,  C10G65/14 ,  C10G73/44 ,  C10G47/00

    CPC classification number: C10G45/58 ,  C10G73/44 ,  C10G2300/1022 ,  C10G2300/301 ,  C10G2400/04 ,  Y10S208/95

    Abstract: The invention relates to a process to prepare a microcrystalline wax and a middle distillate fuel by (a) hydrocracking/hydroisomerizing a Fischer-Tropsch product, wherein the weight ratio of compounds having at least 60 or more carbon atoms and compounds having at least 30 carbon atoms in the Fischer-Tropsch product is at least 0.2 and wherein at least 30 wt % of compounds in the Fischer-Tropsch product have at least 30 carbon atoms, (b) performing one or more distillate separations on the effluent of step (a) to obtain a middle distillate fuel fraction and a microcrystalline wax having an initial boiling point of between 500 and 600° C.

    Abstract translation: 本发明涉及通过（a）费 - 托产物的加氢裂化/加氢异构化制备微晶蜡和中间馏分燃料的方法，其中具有至少60个或更多碳原子的化合物的重量比和具有至少30个碳原子的化合物 费 - 托产物中的原子为至少0.2，并且其中费 - 托产物中至少30wt％的化合物具有至少30个碳原子，（b）在步骤（a）的流出物上进行一种或多种馏出物分离， 以获得中间馏分燃料馏分和初始沸点为500-600℃的微晶蜡。

    Process for preparing a microcrystalline wax
    36.
    发明申请
    Process for preparing a microcrystalline wax 审中-公开
    微晶蜡的制备方法

    公开(公告)号：US20040199040A1

    公开(公告)日：2004-10-07

    申请号：US10480583

    申请日：2003-12-12

    Inventor： Arend Hoek ,  Hendrik Schadenberg

    IPC: C07C005/23 ,  C07C005/25

    CPC classification number: C10G45/62 ,  C10G73/44 ,  C10G2300/1022 ,  C10G2300/301 ,  C10G2300/4018 ,  C10G2400/10

    Abstract: A process to prepare a microcrystalline wax by contacting under hydroisomerisation conditions a feed, having at least 80 wt % of normal-paraffins and having a congealing point of above 60 null C., with a catalyst having a noble metal and a porous silica-alumina carrier.

    Abstract translation: 通过在加氢异构化条件下使具有至少80重量％的正链烷烃和凝结点高于60℃的进料与具有贵金属和多孔二氧化硅 - 氧化铝的催化剂接触来制备微晶蜡的方法 载体

    Catalytic refining process for tank bottoms wax
    38.
    发明授权
    Catalytic refining process for tank bottoms wax 失效
    罐底蜡的催化精制工艺

    公开(公告)号：US4148711A

    公开(公告)日：1979-04-10

    申请号：US812795

    申请日：1977-07-05

    Applicant: Clinton H. Holder

    Inventor： Clinton H. Holder

    IPC: C10G73/44 ,  C10G43/02

    CPC classification number: C10G73/44

    Abstract: High melting, deoiled and mildly deasphalted tank bottoms wax is catalytically refined in two stages using a catalyst comprising nickel molybdate on alumina. The first stage is maintained at a temperature at least about 50.degree. F. higher than the second stage and the temperature in the second stage is allowed to go no higher than about 575.degree. F. Hydrofined wax product from the second stage is recycled back into same and the temperature in the first stage is periodically increased in order to counteract deactivation of the catalyst. By using a judicious combination of process conditions, unrefined high melting tank bottoms microwax stocks can be made into high quality, high melting point microwax having excellent color and meeting FDA purity requirements.

    Abstract translation: 使用包含氧化钼上的钼酸镍的催化剂在两个阶段催化精炼高熔点，脱油和轻度脱沥青罐底部蜡。 第一阶段保持在比第二阶段高至少约50°F的温度，第二阶段的温度不高于约575°F。来自第二阶段的加氢精制蜡产品被再循环回 相同，并且周期性地增加第一阶段中的温度以抵消催化剂的失活。 通过使用工艺条件的合理组合，未精制的高熔点底部微量油可以制成高品质，高熔点的微蜡，具有优异的颜色，符合FDA的纯度要求。

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